CN106757175A - Electrolysis ore electrolytic cell - Google Patents

Electrolysis ore electrolytic cell Download PDF

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Publication number
CN106757175A
CN106757175A CN201611066552.8A CN201611066552A CN106757175A CN 106757175 A CN106757175 A CN 106757175A CN 201611066552 A CN201611066552 A CN 201611066552A CN 106757175 A CN106757175 A CN 106757175A
Authority
CN
China
Prior art keywords
muck
ore
cell body
roller group
inwall
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN201611066552.8A
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Chinese (zh)
Inventor
蒋顺洪
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Chongqing Xinchuanta Industry Co Ltd
Original Assignee
Chongqing Xinchuanta Industry Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Chongqing Xinchuanta Industry Co Ltd filed Critical Chongqing Xinchuanta Industry Co Ltd
Priority to CN201611066552.8A priority Critical patent/CN106757175A/en
Publication of CN106757175A publication Critical patent/CN106757175A/en
Pending legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25CPROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
    • C25C7/00Constructional parts, or assemblies thereof, of cells; Servicing or operating of cells
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25CPROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
    • C25C1/00Electrolytic production, recovery or refining of metals by electrolysis of solutions
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

Abstract

The present invention relates to be electrolysed field, specifically related to a kind of electrolysis ore electrolytic cell, including cell body, positive plate, minus plate, electrolyte membrane, essentially consists in, and cell body bottom is provided with ore crushing apparatus, ore crushing apparatus include muck roller group and muck motor, muck motor is located at outside cell body, and muck motor drives the muck roller group inwardly to rotate, and muck roller group periphery is provided with intermeshing muck tooth;The relative two side of cell body is divided into inner and outer wall, is discharging channel between inwall and the outer wall, and inwall bottom is located at muck roller group top, and inside top is provided with discharge gate.The present invention is realized ore processing into the technique of miberal powder and merging for electrolysis process, effectively raises the electrolytic efficiency of ore, while having saved production and processing cost.

Description

Electrolysis ore electrolytic cell
Technical field
The present invention relates to be electrolysed field, and in particular to one kind electrolysis ore electrolytic cell.
Background technology
Cell body is relatively more crucial equipment in electrolysis field, and the electrolysis to solution is relatively more at present, and to some ore deposits The electrolysis of stone is relatively fewer.In mineral industry, it usually needs the metal in ore is separated, because current technology is to electricity The Technical comparing for solving solution is ripe, so generally needing that ore first is prepared into electrolyte in separation process, then carries out again Electrolytic separation.Ore is prepared into electrolyte needs multiple procedure of processings, and cost is higher, is also deposited during preparation In certain loss so that production efficiency is relatively low.
At present, the electrolytic method using ore pulp is relatively more, in-pulp electrolysis substantially be exactly in cell body addition miberal powder and Corresponding acid so that miberal powder is reacted with acid solution, so as to obtain electrolyte, and effect by anode and negative electrode carries out electricity Solution.It is substantial, and miberal powder is carried out simultaneously with the reaction and electrolysis of acid solution, and such operation enormously simplify and be carried from ore The technique for taking metal, has saved cost, improves production efficiency.But ore deposit is broken into miberal powder, certain technique is also related to, and In the prior art, cell body be not met by electrolysis while can also ore processing into powder requirement;Conventional cell body is also Have the shortcomings that shock resistance is poor.
The content of the invention
The electrolysis ore electrolytic cell that ore is crushed can be realized it is an object of the invention to provide a kind of.
To achieve these goals, base case used is to be electrolysed ore electrolytic cell, including cell body, and positive plate is cloudy Pole plate, electrolyte membrane is essentially consisted in, and cell body bottom is provided with ore crushing apparatus, and ore crushing apparatus include muck roller group and muck motor, Muck motor is located at outside cell body, and muck motor drives the muck roller group inwardly to rotate, and muck roller group periphery is provided with intermeshing Muck tooth;The relative two side of cell body is divided into inner and outer wall, is discharging channel, inwall bottom between inwall and the outer wall Positioned at muck roller group top, inside top is provided with discharge gate.
The operation principle and beneficial effect of base case:By setting ore crushing apparatus inside cell body, realize ore and exist Crushing in cell body, compared with prior art, the technique for further reducing ore processing, so as to save cost, improves The applicability of electroplating bath.Ore crushing apparatus use and muck tooth are set in muck roller group, and installed in cell body bottom, effect is to work as Ore enters when in cell body, can down drop, after falling in muck roller group, due to the squeezing effect between muck roller group, ore deposit Stone is squeezed into powder, and corresponding electrolyte is obtained so as to be easy to acid solution react.In cell body transfer roller groups periphery to Two side is divided into outer wall and inwall, and inwall is located at muck roller group top, and height is corresponding to its diameter, and inwall top is provided with discharge Mouthful, due to the continuous rotation of muck roller group so that mineral dust after crushing is as acid solution is together between inner and outer wall Discharging channel is kicked up upwards, is then flowed out from the discharge gate at top, so as to timely discharge the ore for being accumulated in cell body bottom Powder, also therefore cell body has been internally formed an interior circulation for electrolyte, it is achieved thereby that the stirring action of inside so that formed Ore pulp suspension is realized in cell body, improve the amount of electrolyte of cell body;In addition, by using the resource in system, realizing The saving of resource, improves the utilization rate of resource, so as to further save cost.
Base case is optimized and obtains prioritization scheme 1, for gap coordinates between the muck tooth of muck roller group periphery.Effect Fruit is that while being crushed to ore, can close a certain amount of acid solution by using the cavity volume formed in engagement, It is discharged to muck roller group bottom, accumulate the discharge that more acid solutions are easy to mineral dust.
Prioritization scheme 1 is optimized and obtains prioritization scheme 2, cell body bottom is provided with roller groove corresponding with muck roller group.Effect Fruit is that will not form dead angle in cell body bottom, is easy to the mineral dust to be formed to be kicked up along roller groove when muck roller group is rotated, So as to be conducive to discharge.
Base case and prioritization scheme 1,2 are optimized respectively and obtains prioritization scheme 3, cell body top is provided with multiple can pacify The pole plate draw-in groove of loading electrode plate.Effect is that positive plate and minus plate can as needed adjust installation when ore is electrolysed On corresponding pole plate draw-in groove so that the distance between positive plate and minus plate become adjustable, so as to form different size of Electrolysis chamber.
Prioritization scheme 3 is optimized and obtains prioritization scheme 4, reinforcement is provided with outside cell body.Effect is so that cell body More firm, cracky, does not increase service life.
Base case and prioritization scheme 1,2 are optimized respectively and obtains prioritization scheme 5, cell body is manufactured for insulating materials. Effect is that, in electrolysis, cell body will not be grounded and be communicated with the earth, so as to avoid leakage loss during electrolysis, reduce consumption Electricity.
Brief description of the drawings
Fig. 1 is the front view of invention electrolysis ore electrolytic cell;
Fig. 2 is the left view of invention electrolysis ore electrolytic cell;
Fig. 3 is the top view of invention electrolysis ore electrolytic cell.
Specific embodiment
Embodiment
Drawing reference numeral explanation:Cell body 1, positive plate 2, minus plate 3, electrolyte membrane 4, muck roller group 5, muck motor 6, reinforcement Muscle 7, inwall 8, roller groove 9, muck tooth 10, draw-in groove 11.
As shown in Figure 1, Figure 2 and Figure 3, ore electrolytic cell, including cell body 1 are electrolysed, muck is installed in the bottom of cell body 1 Roller group 5, the length of muck roller group 5 is mutually fitted with the length of cell body 1, and intermeshing muck tooth 10, engagement are housed in muck roller group 5 Mode be gap coordinate.A muck motor 6 is installed in the outside of cell body 1, the muck motor 6 turns with muck roller group 5 Axle is connected, and the bottom of cell body 1 coordinates the roller groove 9 for being provided with and mutually being fitted with muck roller group 5.It is installed with the top of muck roller group 5 Two pieces of inwalls 8, the bottom of inwall 8 is slightly above the side of muck roller group 5, and the top of inwall 8 is provided with discharge gate.The top of cell body 1 Relative both sides are provided with mutually symmetrical with draw-in groove 11, and positive plate 2 and minus plate 3 are alternate installed in different both sides respectively, in sun Electrolyte membrane 4 is installed between pole plate 2 and minus plate 3.Each side of cell body 1 is fixed with cross one another reinforcement 7.Manufacture Material used by cell body 1 is fiberglass.
When ore is electrolysed, muck motor 6 is started first, then ore is put into fall under cell body 1, ore it is broken When in ore deposit roller group 5, extruding for muck roller group 5 will be subject to, crushes ore, and be expressed in the roller groove 9 below muck roller group 5. Due to the clearance meshing relation between muck roller group 5 so that it constantly arranges downwards acid solution in motion, can now form one The system of similar gear pump discharge opeing so that pulverized ore is taken away by acid solution, and the discharging channel between outer wall and inwall 8 Flow up, then discharged from the discharge gate on the top of inwall 8, so as to internally form a circulatory system.Ore deposit after crushing Stone is easily reacted with acid solution, obtains electrolyte, as positive plate 2 and minus plate 3 are constantly acted on so that in positive plate 2 Continuous precipitating metal near acid solution, minus plate 3 is nearby constantly produced, and by the effect of electrolyte membrane 4, by the filtering of its slag Fall.By this while powder ore, a circulatory system for acid solution is also internally formd, so that in cell body 1 Ore pulp produced by interior is realized suspending, and realizes the reasonable utilization of resource, has saved production cost, improves production efficiency.
Above-described is only embodiments of the invention, and the general knowledge such as known concrete structure or characteristic is not made herein in scheme Excessive description.It should be pointed out that for a person skilled in the art, on the premise of structure of the present invention is not departed from, can be with Some deformations and improvement are made, these should also be considered as protection scope of the present invention, these are implemented all without the influence present invention Effect and practical applicability.This application claims protection domain should be defined by the content of its claim, in specification Specific embodiment etc. records the content that can be used for explaining claim.

Claims (6)

1. ore electrolytic cell, including cell body are electrolysed(1), multiple positive plates(2), multiple minus plates(3)And electrolyte membrane(4), Positive plate setting alternate with the minus plate, it is characterised in that:The cell body(1)Bottom is provided with ore crushing apparatus, described Ore crushing apparatus include muck roller group(5)With muck motor(6), the muck motor(6)Positioned at cell body(1)Outward, muck motor(6) Drive the muck roller group(5)Rotate, muck roller group(5)Periphery is provided with intermeshing muck tooth(10);Cell body(1)It is interior relative One group of side wall be divided into inwall(8)And outer wall, the inwall(8)It is discharging channel, inwall and the outer wall between(8)Bottom position In muck roller group(5)Top, is provided with discharge gate at the top of inwall.
It is 2. according to claim 1 to be electrolysed ore electrolytic cell, it is characterised in that:The muck roller group(5)Periphery it is broken Ore deposit tooth(10)Between be gap coordinate.
It is 3. according to claim 2 to be electrolysed ore electrolytic cell, it is characterised in that:The cell body(1)Bottom be provided with it is broken Ore deposit roller group(5)Corresponding roller groove(9).
4. the electrolysis ore electrolytic cell according to claims 1 to 3 any one, it is characterised in that:The cell body(1)Top Portion is provided with multiple pole plate draw-in grooves that can install battery lead plate(11).
It is 5. according to claim 4 to be electrolysed ore electrolytic cell, it is characterised in that:The cell body(1)Outside is provided with reinforcement Muscle(7).
6. the electrolysis ore electrolytic cell according to claims 1 to 3 any one, it is characterised in that:The cell body(1)For Insulating materials is manufactured.
CN201611066552.8A 2016-11-28 2016-11-28 Electrolysis ore electrolytic cell Pending CN106757175A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201611066552.8A CN106757175A (en) 2016-11-28 2016-11-28 Electrolysis ore electrolytic cell

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201611066552.8A CN106757175A (en) 2016-11-28 2016-11-28 Electrolysis ore electrolytic cell

Publications (1)

Publication Number Publication Date
CN106757175A true CN106757175A (en) 2017-05-31

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201611066552.8A Pending CN106757175A (en) 2016-11-28 2016-11-28 Electrolysis ore electrolytic cell

Country Status (1)

Country Link
CN (1) CN106757175A (en)

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1082616A (en) * 1992-08-01 1994-02-23 杨春山 Electric deposition of copper powder and extracting cupric oxide ore by carbon amino method technology
CN1139704A (en) * 1996-03-22 1997-01-08 核工业北京化工冶金研究院 Method for extracting copper from ore
CN2625395Y (en) * 2003-05-01 2004-07-14 鞍山科技大学 Dynamic electrolyzing machine for regenerating and treating waste and old hard alloy
CN201179455Y (en) * 2008-04-16 2009-01-14 抚顺铝业有限公司 Anti-loose pair-roll machine
CN104313650A (en) * 2014-11-25 2015-01-28 吉首大学 Mechanical agitation type ore pulp electrolytic cell
CN105018965A (en) * 2015-07-28 2015-11-04 重庆新川塔实业股份有限公司 Electrolytic tank for manganese element

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1082616A (en) * 1992-08-01 1994-02-23 杨春山 Electric deposition of copper powder and extracting cupric oxide ore by carbon amino method technology
CN1139704A (en) * 1996-03-22 1997-01-08 核工业北京化工冶金研究院 Method for extracting copper from ore
CN2625395Y (en) * 2003-05-01 2004-07-14 鞍山科技大学 Dynamic electrolyzing machine for regenerating and treating waste and old hard alloy
CN201179455Y (en) * 2008-04-16 2009-01-14 抚顺铝业有限公司 Anti-loose pair-roll machine
CN104313650A (en) * 2014-11-25 2015-01-28 吉首大学 Mechanical agitation type ore pulp electrolytic cell
CN105018965A (en) * 2015-07-28 2015-11-04 重庆新川塔实业股份有限公司 Electrolytic tank for manganese element

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Application publication date: 20170531

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